JP2684767B2 - Method for producing aminocyanacetamide - Google Patents
Method for producing aminocyanacetamideInfo
- Publication number
- JP2684767B2 JP2684767B2 JP1120230A JP12023089A JP2684767B2 JP 2684767 B2 JP2684767 B2 JP 2684767B2 JP 1120230 A JP1120230 A JP 1120230A JP 12023089 A JP12023089 A JP 12023089A JP 2684767 B2 JP2684767 B2 JP 2684767B2
- Authority
- JP
- Japan
- Prior art keywords
- ester
- acid
- acid ester
- give
- aminocyanoacetic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- JRWAUKYINYWSTA-UHFFFAOYSA-N 2-amino-2-cyanoacetamide Chemical compound N#CC(N)C(N)=O JRWAUKYINYWSTA-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- -1 cyanoacetic acid ester Chemical class 0.000 claims abstract description 30
- 238000000034 method Methods 0.000 claims abstract description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 16
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 6
- MLIREBYILWEBDM-UHFFFAOYSA-N anhydrous cyanoacetic acid Natural products OC(=O)CC#N MLIREBYILWEBDM-UHFFFAOYSA-N 0.000 claims abstract description 5
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 25
- 239000003054 catalyst Substances 0.000 claims description 17
- 229910052697 platinum Inorganic materials 0.000 claims description 13
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 9
- 229910052739 hydrogen Inorganic materials 0.000 claims description 9
- 239000001257 hydrogen Substances 0.000 claims description 9
- 238000005984 hydrogenation reaction Methods 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 7
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 2
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims description 2
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical group [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 claims description 2
- 229910003446 platinum oxide Inorganic materials 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 235000012239 silicon dioxide Nutrition 0.000 claims description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims 2
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 claims 2
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical compound C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 claims 1
- 229910000019 calcium carbonate Inorganic materials 0.000 claims 1
- 238000002360 preparation method Methods 0.000 abstract description 6
- 239000012467 final product Substances 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Natural products CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 35
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 26
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- 239000000047 product Substances 0.000 description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 14
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 239000000706 filtrate Substances 0.000 description 9
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- 239000011541 reaction mixture Substances 0.000 description 8
- LPXPTNMVRIOKMN-UHFFFAOYSA-M sodium nitrite Chemical compound [Na+].[O-]N=O LPXPTNMVRIOKMN-UHFFFAOYSA-M 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 238000000921 elemental analysis Methods 0.000 description 6
- ZIUSEGSNTOUIPT-UHFFFAOYSA-N ethyl 2-cyanoacetate Chemical compound CCOC(=O)CC#N ZIUSEGSNTOUIPT-UHFFFAOYSA-N 0.000 description 6
- VNJOEUSYAMPBAK-UHFFFAOYSA-N 2-methylbenzenesulfonic acid;hydrate Chemical compound O.CC1=CC=CC=C1S(O)(=O)=O VNJOEUSYAMPBAK-UHFFFAOYSA-N 0.000 description 5
- 239000005457 ice water Substances 0.000 description 5
- 229960000583 acetic acid Drugs 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- ZTUBRMAHOKWHCL-UHFFFAOYSA-N methyl 2-cyano-2-hydroxyiminoacetate Chemical compound COC(=O)C(=NO)C#N ZTUBRMAHOKWHCL-UHFFFAOYSA-N 0.000 description 4
- 239000012044 organic layer Substances 0.000 description 4
- 238000001953 recrystallisation Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 235000010288 sodium nitrite Nutrition 0.000 description 4
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 3
- 239000012362 glacial acetic acid Substances 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- ANGDWNBGPBMQHW-UHFFFAOYSA-N methyl cyanoacetate Chemical compound COC(=O)CC#N ANGDWNBGPBMQHW-UHFFFAOYSA-N 0.000 description 3
- 229910052938 sodium sulfate Inorganic materials 0.000 description 3
- 235000011152 sodium sulphate Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- KDCGOANMDULRCW-UHFFFAOYSA-N 7H-purine Chemical compound N1=CNC2=NC=NC2=C1 KDCGOANMDULRCW-UHFFFAOYSA-N 0.000 description 2
- 229910000497 Amalgam Inorganic materials 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- NQVKIVQYIPYDAG-UHFFFAOYSA-N benzyl 2-cyano-2-hydroxyiminoacetate Chemical compound ON=C(C#N)C(=O)OCC1=CC=CC=C1 NQVKIVQYIPYDAG-UHFFFAOYSA-N 0.000 description 2
- JYGRVMQGWVVHJE-UHFFFAOYSA-N ethyl 2-amino-2-cyanoacetate Chemical compound CCOC(=O)C(N)C#N JYGRVMQGWVVHJE-UHFFFAOYSA-N 0.000 description 2
- LCFXLZAXGXOXAP-UHFFFAOYSA-N ethyl 2-cyano-2-hydroxyiminoacetate Chemical compound CCOC(=O)C(=NO)C#N LCFXLZAXGXOXAP-UHFFFAOYSA-N 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 125000002088 tosyl group Chemical group [H]C1=C([H])C(=C([H])C([H])=C1C([H])([H])[H])S(*)(=O)=O 0.000 description 2
- RQMFZXWHCJWDQQ-UHFFFAOYSA-N 2-amino-2-cyanoacetic acid Chemical class N#CC(N)C(O)=O RQMFZXWHCJWDQQ-UHFFFAOYSA-N 0.000 description 1
- MLIREBYILWEBDM-UHFFFAOYSA-M 2-cyanoacetate Chemical compound [O-]C(=O)CC#N MLIREBYILWEBDM-UHFFFAOYSA-M 0.000 description 1
- IZVKFRHZQHXQTF-UHFFFAOYSA-N C(#N)ON(O)OC#N Chemical compound C(#N)ON(O)OC#N IZVKFRHZQHXQTF-UHFFFAOYSA-N 0.000 description 1
- 229910000564 Raney nickel Inorganic materials 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- ZIUKUZLYSVRLMN-UHFFFAOYSA-N [cyanato(ethoxy)amino] cyanate Chemical compound C(C)ON(OC#N)OC#N ZIUKUZLYSVRLMN-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- BIAHCDGTHBPHIW-UHFFFAOYSA-N benzyl 2-amino-2-cyanoacetate Chemical compound N#CC(N)C(=O)OCC1=CC=CC=C1 BIAHCDGTHBPHIW-UHFFFAOYSA-N 0.000 description 1
- WDANMHJYKHSJPP-UHFFFAOYSA-N benzyl 2-hydroxyiminoacetate Chemical compound C(C1=CC=CC=C1)OC(C=NO)=O WDANMHJYKHSJPP-UHFFFAOYSA-N 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 150000001733 carboxylic acid esters Chemical class 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004643 cyanate ester Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- AFVFQIVMOAPDHO-UHFFFAOYSA-M methanesulfonate group Chemical class CS(=O)(=O)[O-] AFVFQIVMOAPDHO-UHFFFAOYSA-M 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 150000004702 methyl esters Chemical class 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000000802 nitrating effect Effects 0.000 description 1
- 150000002826 nitrites Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000003901 oxalic acid esters Chemical class 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- CPNGPNLZQNNVQM-UHFFFAOYSA-N pteridine Chemical compound N1=CN=CC2=NC=CN=C21 CPNGPNLZQNNVQM-UHFFFAOYSA-N 0.000 description 1
- PBMFSQRYOILNGV-UHFFFAOYSA-N pyridazine Chemical compound C1=CC=NN=C1 PBMFSQRYOILNGV-UHFFFAOYSA-N 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 125000003944 tolyl group Chemical group 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C255/00—Carboxylic acid nitriles
- C07C255/01—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms
- C07C255/24—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms containing cyano groups and singly-bound nitrogen atoms, not being further bound to other hetero atoms, bound to the same saturated acyclic carbon skeleton
- C07C255/28—Carboxylic acid nitriles having cyano groups bound to acyclic carbon atoms containing cyano groups and singly-bound nitrogen atoms, not being further bound to other hetero atoms, bound to the same saturated acyclic carbon skeleton containing cyano groups, amino groups and carboxyl groups, other than cyano groups, bound to the carbon skeleton
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
- Peptides Or Proteins (AREA)
- Cephalosporin Compounds (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は、工業的に実施できるアミノシアンアセトア
ミドの新規な製造方法に関する。The present invention relates to a novel process for producing aminocyanacetamide which can be industrially carried out.
アミノシアンアセトアミドは、たとえばイミダゾー
ル、ピリダジン、プリンまたはプテリジンなどを製造す
るための、重要な中間体である。Aminocyanacetamide is a key intermediate for the production of eg imidazole, pyridazine, purine or pteridine.
アミノシアノ酢酸エステルの製造に関しては、多くの
方法が知られている。Many methods are known for the production of aminocyanoacetic acid esters.
西ドイツ特許公開公報第2700733号には、ヒドロキシ
イミノシアノ酢酸エチルをラネーニッケル触媒で水素化
してアミノシアノ酢酸エチルにする方法が開示されてい
る。この方法で得られる収率は65%である。West German Patent Publication No. 2700733 discloses a method of hydrogenating ethyl hydroxyiminocyanoacetate with Raney nickel catalyst to give ethyl aminocyanoacetate. The yield obtained by this method is 65%.
分離された生成物の収率は低く、品質が良くないうえ
に、触媒の再生および循環使用時に比較的多量の触媒が
消費されるという欠点がある。このような消費は、工業
的実施化には不適である。The yields of the separated products are low, the quality is poor, and a relatively large amount of catalyst is consumed during the regeneration and recycling of the catalyst. Such consumption is unsuitable for industrial implementation.
ローゲマンらの方法〔Logeman et al,Chem,and Ind.
(1980),541〕によれば、ヒドロキシイミノシアノ酢酸
エチルをエタノール溶媒を用いて亜ニチオン酸ナトリウ
ムと反応させ、アミノシアノ酢酸エチルを収率81%(粗
製収率)で得ることができる。Logeman et al, Chem, and Ind.
(1980), 541], ethyl hydroxyiminocyanoacetate can be reacted with sodium dithionite using an ethanol solvent to obtain ethylaminocyanoacetate in a yield of 81% (crude yield).
この方法の欠点は、硫酸塩の沈澱が生じることと、引
火性のエーテルを使用することである。塩の沈澱という
わずらわしい問題のために、この方法は採用し難い。Disadvantages of this method are the occurrence of sulfate precipitation and the use of flammable ethers. This method is difficult to adopt because of the annoying problem of salt precipitation.
また、テーラーらの方法〔Tayler et al,J.Am.Chem.S
oc.98,2301(1976)〕により、ヒドロキシイミノシアノ
酢酸ベンジルエステルをAl−アマルガムおよびエーテル
溶媒を用いてメタンスルホン酸と二段階で反応させて、
アミノシアノ酢酸ベンジルのメタンスルホン酸塩を収率
53%で得ることができる。In addition, the method of Taylor et al. [Tayler et al, J. Am. Chem. S.
oc.98,2301 (1976)], hydroxyiminocyanoacetic acid benzyl ester is reacted with methanesulfonic acid in two steps using Al-amalgam and an ether solvent,
Yield methanesulfonate of benzyl aminocyanoacetate
Can be obtained at 53%.
この方法は、水銀触媒を用いるという厄介な問題を抱
えているから、工業的に採用できないことは議論の余地
がない。Since this method has a troublesome problem of using a mercury catalyst, it cannot be argued that it cannot be industrially adopted.
スミスらの方法〔Smith et al,J.Am.Chem.Soc.76,608
0(1954)〕にも、同様の欠点がある。その方法は、ヒ
ドロキシイミノシアンアセトアミドをAl−アマルガムで
水素化し、直接アミノシアンアセトアミドにするもので
あって、収率は59%である。Smith et al., J. Am. Chem. Soc. 76,608
0 (1954)] also has similar drawbacks. The method involves hydrogenating hydroxyimino cyanacetamide with Al-amalgam to directly give amino cyanacetamide in a yield of 59%.
本発明の課題は、上記のような欠点がなく、入手容易
な出発原点からアミノシアンアセトアミドを工業的に、
かつできるだけ環境汚染を少なくして製造することので
きる方法を提供することにある。The subject of the present invention is not the above-mentioned drawbacks, industrially from the starting origin easily available aminocyanacetamide,
Another object of the present invention is to provide a method that can be manufactured with minimal environmental pollution.
この課題は、請求項1に記載の方法により達成でき
る。This object can be achieved by the method according to claim 1.
本発明の方法の出発点は、取扱いが容易なシアノ酢酸
エステルを用いることである。本発明方法には、メチル
−、エチル−、プロピル−、ブチル−またはt−ブチル
エステルなどのC1〜C4アルキルエステルが好適に使用さ
れる。The starting point for the process of the present invention is the use of cyanoacetates, which are easy to handle. The method of the present invention, methyl -, ethyl -, propyl -, butyl - or C 1 -C 4 alkyl esters, such as t- butyl ester are preferably used.
シアノ酢酸エステルは、第一段階で既知の方法〔たと
えば、G.Duguay,J.Heterocycl.Chem.17,767(1980)〕
によりニトロ化して、ヒドロキシイミノシアノ酢酸エス
テルとする。ニトロ化剤としては、通常のアルカリ金属
の亜硝酸塩、とくに亜硝酸ナトリウムを用いる。反応は
酸性媒体中で行なう。The cyanoacetic acid ester can be prepared by a known method in the first step [eg, G. Duguay, J. Heterocycl. Chem. 17 , 767 (1980)].
To give hydroxyiminocyanoacetic acid ester. Usual nitrites of alkali metals, especially sodium nitrite, are used as nitrating agents. The reaction is carried out in an acidic medium.
生じたヒドロキシイミノシアン酢酸エステルは通常は
有機層に移行する。必要に応じてこれを分離してもよい
が、次工程に直接用いるのが好ましい。The resulting hydroxyimino cyanate ester usually migrates to the organic layer. This may be separated if necessary, but it is preferably used directly in the next step.
次工程、すなわちヒドロキシイミノシアノ酢酸エステ
ルのアミノシアノ酢酸エステルへの水素化は、白金触媒
の存在下に水素を用いて行なう。好ましい白金触媒は、
炭素、酸化アルミニウム、二酸化ケイ素、硫酸バリウム
または炭酸カリウムなど微粉末状の担体に白金を1〜20
重量%担持させたもの、または酸化白金である。中で
も、白金を3〜10重量%炭素に担持させたものがすぐれ
ている。The next step, the hydrogenation of hydroxyiminocyanoacetic acid ester to aminocyanoacetic acid ester, is carried out using hydrogen in the presence of a platinum catalyst. A preferred platinum catalyst is
1 to 20 platinum on a fine powder carrier such as carbon, aluminum oxide, silicon dioxide, barium sulfate or potassium carbonate
It is one supported by weight% or platinum oxide. Among them, the one in which platinum is supported on carbon in an amount of 3 to 10% by weight is excellent.
白金触媒の使用量は、ヒドロキシイミノシアノ酢酸エ
ステルに対し3〜30重量、とくに10〜15重量%とするの
が好ましい。The platinum catalyst is used in an amount of 3 to 30% by weight, preferably 10 to 15% by weight, based on the hydroxyiminocyanoacetic acid ester.
水素化の条件は、経験によれば圧力1〜100バール、
とくに6〜10バールおよび温度0〜40℃、とくに室温付
近が好ましい。The hydrogenation conditions are, according to experience, pressures of 1-100 bar,
Especially preferred is 6-10 bar and temperature 0-40 ° C, especially around room temperature.
反応には低沸点の有機溶媒を用いるのが有利である。
このような溶媒としては、エタノールなどの低級脂肪族
アルコール、酢酸エチルなどの低級カルボン酸エステ
ル、酢酸などの低級カルボン酸が挙げられる。It is advantageous to use an organic solvent having a low boiling point for the reaction.
Examples of such a solvent include lower aliphatic alcohols such as ethanol, lower carboxylic acid esters such as ethyl acetate, and lower carboxylic acids such as acetic acid.
反応時間は、圧力、温度および触媒量によって異なる
が、0.5〜10時間程度である。The reaction time varies depending on the pressure, the temperature and the amount of catalyst, but is about 0.5 to 10 hours.
本発明の製造方法の大きな利点は、反応終了後に白金
触媒を回収し、次の水素化にこれを再使用できることで
ある。The great advantage of the production method of the present invention is that the platinum catalyst can be recovered after the reaction and can be reused for the next hydrogenation.
得られたアミノシアノ酢酸エステルは、反応溶液から
分離してもよいが、分離せずに直接アンモニアと反応さ
せて、目的生成物であるアミノシアノアセトアミドとす
ることができる。The obtained aminocyanoacetic acid ester may be separated from the reaction solution, but can be directly reacted with ammonia without separation to give the desired product aminocyanoacetamide.
アミノシアンアセトアミドへの転化は、濃度10〜40重
量%のアンモニア水を用いて、−20〜30℃、好ましくは
0〜5℃の温度で行なう。The conversion to aminocyanacetamide is carried out using ammonia water having a concentration of 10 to 40% by weight at a temperature of -20 to 30 ° C, preferably 0 to 5 ° C.
アンモニアとアミノシアノ酢酸エステルのモル比は、
30:1〜1:1の間で選ぶことができる。好ましい範囲は10:
1〜5:1である。The molar ratio of ammonia to aminocyanoacetic ester is
You can choose between 30: 1 and 1: 1. The preferred range is 10:
1 to 5: 1.
第1段階の反応には溶媒を用いるが、溶媒を用いずに
アンモニア水だけを使用して、これに代えることができ
る。Although a solvent is used for the reaction in the first step, it is possible to replace it by using only aqueous ammonia without using a solvent.
生成したアミノシアンアセトアミドは、通常の処理を
行なうことにより、純度98%以上の高温位のものがシア
ン酢酸エステル基準で70%以上の収率で得られる。The produced aminocyanacetamide can be obtained in a yield of 70% or more on the basis of cyanoacetate with a purity of 98% or more at a high temperature by performing usual treatment.
アミノシアノ酢酸エステルは、前述したように種々の
合成品の重要な中間体であるが、それ自体は保存安定性
が乏しいから、水素化反応の終了後に反応溶液に酸を添
加して、アミノシアノ酢酸エステルを塩の形態にするこ
とが好ましい。このような塩としては、トシル塩、シュ
ウ酸塩またはメタンスルホン酸塩などがあり、とくにト
シル塩が好ましい。As mentioned above, aminocyanoacetic acid ester is an important intermediate of various synthetic products, but since it has poor storage stability, it is necessary to add an acid to the reaction solution after completion of the hydrogenation reaction to give aminocyanoacetic acid ester. Is preferably in the form of a salt. Such salts include tosyl salts, oxalates or methanesulfonates, and tosyl salts are particularly preferred.
これらの塩は、保存安定性がよく、取扱も容易で、高
純度のものを製造することができる。These salts have good storage stability, are easy to handle, and can be produced in high purity.
実施例1 シアノ酢酸エチルからヒドロキシイミノシアン酢酸エチ
ルの製造 シアノ酢酸エチル113.7g(1.0モル)と亜硝酸ナトリ
ウム83.2g(1.2モル)を900mlの氷水に溶媒した。この
溶液に氷酢酸83.0gを、10℃以下で30分間かけて滴下し
た。これを20℃で4時間撹拌した後、濃塩酸100mlを加
え、各150mlの酢酸エチルで4回抽出した。Example 1 Production of ethyl hydroxyimino cyanate from ethyl cyanoacetate 113.7 g (1.0 mol) of ethyl cyanoacetate and 83.2 g (1.2 mol) of sodium nitrite were dissolved in 900 ml of ice water as a solvent. To this solution, 83.0 g of glacial acetic acid was added dropwise at 10 ° C or lower over 30 minutes. This was stirred at 20 ° C. for 4 hours, 100 ml of concentrated hydrochloric acid was added, and the mixture was extracted 4 times with 150 ml of ethyl acetate each.
有機層を各50mlの氷水で4回洗浄し、硫酸ナトリウム
で乾燥し、245gに濃縮した後、4℃で12時間保持した。The organic layer was washed 4 times with 50 ml of ice water each, dried over sodium sulfate, concentrated to 245 g, and kept at 4 ° C. for 12 hours.
沈澱したヒドロキシイミノ酢酸エチルを濾別し、冷酢
酸エチルで洗浄し、乾燥した。The precipitated hydroxyimino ethyl acetate was filtered off, washed with cold ethyl acetate and dried.
その結果、130.6gの生成物が得られた。収率91.9%
(シアノ酢酸エチル基準)、融点129.5〜131℃。As a result, 130.6 g of product was obtained. Yield 91.9%
(Based on ethyl cyanoacetate), melting point 129.5-131 ° C.
元素分析:C5H6N2O3 計算値 C41.75%、H4.25%、N19.11% 実測値 C42.26%、H4.26%、N19.71% 実施例2 ヒドロキシイミノシアノ酢酸エステルからアミノシアノ
酢酸メチルエステル−トシル塩の製造 ヒドロキシイミノシアノ酢酸メチルエステル18.0g
(0.14モル)を200mlのエタノールに溶解し、これを2.7
gの5%Pt/C触媒を用いて、水素圧力10バール、室温の
下で水素化した。反応混合物を濾過し、濾液にトルエン
750mlとともにトルエンスルホン酸一水和物26.9g(0.14
モル)を加えて340gに濃縮した後、4℃で12時間保持し
た。Elemental analysis: C 5 H 6 N 2 O 3 Calculated C41.75%, H4.25%, N19.11% Found C42.26%, H4.26%, N19.71% Example 2 hydroxyimino cyanoacetate Preparation of aminocyanoacetic acid methyl ester-tosyl salt from ester Hydroxyiminocyanoacetic acid methyl ester 18.0 g
Dissolve (0.14 mol) in 200 ml of ethanol and add 2.7
Hydrogenated with g 5% Pt / C catalyst under hydrogen pressure 10 bar at room temperature. The reaction mixture is filtered and the filtrate is toluene.
Toluenesulfonic acid monohydrate 26.9g (0.14
Mol) was added and the mixture was concentrated to 340 g and kept at 4 ° C. for 12 hours.
沈澱したアミノシアノ酢酸メチルエステル−トシル塩
を濾別し、トルエンで洗浄し、乾燥した。The precipitated aminocyanoacetic acid methyl ester-tosyl salt was filtered off, washed with toluene and dried.
その結果、36.9gの生成物が89.7%の収率(ヒドロキ
シイミノシアノ酢酸メチルエステル基準)で得られた。
融点162.5〜164.5℃。As a result, 36.9 g of a product was obtained in a yield of 89.7% (based on hydroxyiminocyanoacetic acid methyl ester).
Melting point 162.5-164.5 ° C.
元素分析:C11H14N2O2S 計算値 C45.80%、H49.2%、N9.65% 実測値 C46.18%、H4.93%、N9.79% 実施例3 ヒドロキシイミノシアン酢酸エチルエステルからアミノ
シアン酢酸エチルエステル−トシル塩の製造 ヒドロキシイミノシアン酢酸エチルエステル20.0g
(0.14モル)を200mlのエタノールに溶解し、2.6gの5
%Pt/C触媒を用いて、水素圧力10バールの下、室温で水
素化した。Elemental analysis: C 11 H 14 N 2 O 2 S Calculated value C45.80%, H49.2%, N9.65% Measured value C46.18%, H4.93%, N9.79% Example 3 Hydroxyiminocyan Production of aminocyanacetic acid ethyl ester-tosyl salt from acetic acid ethyl ester Hydroxyiminocyanacetic acid ethyl ester 20.0 g
Dissolve (0.14 mol) in 200 ml of ethanol and add 2.6 g of 5
Hydrogenation was carried out at room temperature under a hydrogen pressure of 10 bar using a% Pt / C catalyst.
反応混合物を濾過し、濾液にトルエン1200mlとともに
トルエンスルホン酸一水和物26.9g(0.14モル)を加え
て330gに濃縮した後、4℃で12時間保持した。The reaction mixture was filtered, 1200 ml of toluene and 26.9 g (0.14 mol) of toluenesulfonic acid monohydrate were added to the filtrate, and the mixture was concentrated to 330 g and then kept at 4 ° C. for 12 hours.
沈澱したアミノシアノ酢酸エチルエステルートシル塩
を濾別し、トルエンで洗浄し、乾燥した。The precipitated aminocyanoacetic acid ethyl ester tosyl salt was filtered off, washed with toluene and dried.
その結果、40.0gの生成物が93.4%の収率(ヒドロキ
シイミノシアン酢酸エチルエステル基準)で得られた。
融点、128〜130℃。As a result, 40.0 g of the product was obtained in a yield of 93.4% (based on hydroxyimino cyanic acid ethyl ester).
Melting point, 128-130 ° C.
酢酸エチルから再結晶して分離した生成物の融点は13
0〜131℃であった。The product separated by recrystallization from ethyl acetate has a melting point of 13
It was 0 to 131 ° C.
元素分析:C12H16N2O5S 計算値 C47.44%、H5.42%、N9.21% 実測値 C48.00%、H5.37%、N9.33% 実施例4 ヒドロキシイミノシアンベンジルエステルからアミノシ
アノ酢酸ベンジルエステル−トシル塩の製造 ヒドロキシイミノシアノ酢酸ベンジルエステル20.4g
(0.1モル)を200mlのエタノールに溶解し、これを3.1g
の5%Pt/C触媒を用いて、水素圧力10バールの下、室温
で水素化した。反応混合物を濾過し、濾液にトルエンス
ルホン酸一水和物19.2g(0.1モル)を加えて150gに濃縮
し、さらにトルエン400mlを加えて230gに濃縮した後、
4℃で12時間保持した。Elemental analysis: C 12 H 16 N 2 O 5 S Calculated value C47.44%, H5.42%, N9.21% Measured value C48.00%, H5.37%, N9.33% Example 4 Hydroxyiminocyan Preparation of aminocyanoacetic acid benzyl ester-tosyl salt from benzyl ester Hydroxyiminocyanoacetic acid benzyl ester 20.4 g
Dissolve (0.1 mol) in 200 ml ethanol and add 3.1 g
Was hydrogenated at room temperature under 10 bar hydrogen pressure using 5% Pt / C catalyst. The reaction mixture was filtered, 19.2 g (0.1 mol) of toluenesulfonic acid monohydrate was added to the filtrate and concentrated to 150 g, and 400 ml of toluene was further added and concentrated to 230 g,
Hold at 4 ° C for 12 hours.
沈澱したアミノシアノ酢酸ベンジルエステルートシル
塩を濾別し、トルエンで洗浄し、乾燥した。The precipitated aminocyanoacetic acid benzyl ester tosyl salt was filtered off, washed with toluene and dried.
その結果、31.2gの生成物が86.3%の収率(ヒドロキ
シイミノ酢酸ベンジルエステル基準)で得られた。融点
171〜172℃。As a result, 31.2 g of the product was obtained in a yield of 86.3% (based on hydroxyiminoacetic acid benzyl ester). Melting point
171-172 ° C.
イソプロパノールから再結晶して分離した生成物の融
点は173〜174℃であった。The melting point of the product separated by recrystallization from isopropanol was 173-174 ° C.
元素分析:C17H18N2O5S 計算値 C55.6%、H4.95%、N7.82% 実測値 C56.38%、H5.01%、N7.73% 実施例5 ヒドロキシイミノシアノ酢酸−t−ブチルエステルから
アミノシアノ酢酸−t−ブチルエステル−トシル塩の製
造 ヒドロキシイミノシアノ酢酸−t−ブチルエステル2
1.3g(0.1gモル)を200mlのエタノールに溶解し、これ
を3.2gの5%Pt/C触媒を用いて、水素圧力10バールの
下、室温で水素化した。反応混合物を濾過し、濾液にト
ルエン500mlとともにトルエンスルホン酸一水和物19.0g
(0.1モル)を加えて204gに濃縮した後、4℃で12時間
保持した。Elemental analysis: C 17 H 18 N 2 O 5 S Calculated value C55.6%, H4.95%, N7.82% Measured value C56.38%, H5.01%, N7.73% Example 5 Hydroxyiminocyano Preparation of aminocyanoacetic acid-t-butyl ester-tosyl salt from acetic acid-t-butyl ester Hydroxyiminocyanoacetic acid-t-butyl ester 2
1.3 g (0.1 g mol) was dissolved in 200 ml of ethanol and hydrogenated with 3.2 g of 5% Pt / C catalyst under hydrogen pressure of 10 bar at room temperature. The reaction mixture was filtered, and the filtrate was mixed with toluene (500 ml) and toluenesulfonic acid monohydrate (19.0 g).
(0.1 mol) was added, the mixture was concentrated to 204 g, and then kept at 4 ° C. for 12 hours.
沈澱したアミノシアノ酢酸−t−ブチルエステル−ト
シル塩を濾別し、トルエンで洗浄し、乾燥した。The precipitated aminocyanoacetic acid-t-butyl ester-tosyl salt was filtered off, washed with toluene and dried.
その結果、16.2gの生成物が51.1%の収率(ヒドロキ
シイミノシアン酢酸−t−ブチルエステル基準)で得ら
れた。融点124〜126℃。As a result, 16.2 g of a product was obtained in a yield of 51.1% (based on hydroxyimino cyanic acid-t-butyl ester). 124-126 ° C.
酢酸エチル/エタノール(3:1)から再結晶して分離
した生成物の融点は128〜129.5℃であった。The melting point of the product separated by recrystallization from ethyl acetate / ethanol (3: 1) was 128-129.5 ° C.
元素分析:C14H20N2O5S 計算値 C51.15%、H6.21%、N8.65% 実測値 C51.24%、H6.14%、N8.54% 実施例6 シアノ酢酸エチルエステルからアミノシアノ酢酸エチル
エステル−トシル塩の製造 シアノ酢酸エチルエステル17.1g(0.1モル)および亜
硝酸ナトリウム12.4g(0.18モル)を135mlの氷水に溶解
し、これに氷酢酸12.5g(0.21モル)を10℃で10分間か
けて滴下した。この溶液を20℃で1時間撹拌し、濃塩酸
15mlを加えて各50mlの酢酸エチルで4回抽出した。有機
層を各15mlの氷水で洗浄して中性にし、硫酸ナトリウム
で乾燥した後、200gに濃縮した。この溶液を3.2gのPt/C
(5%)触媒を用い、水素圧力10バールの下、室温で水
素化した。Elemental analysis: C 14 H 20 N 2 O 5 S Calculated value C51.15%, H6.21%, N8.65% Measured value C51.24%, H6.14%, N8.54% Example 6 Ethyl cyanoacetate Preparation of aminocyanoacetic acid ethyl ester-tosyl salt from ester 17.1 g (0.1 mol) of cyanoacetic acid ethyl ester and 12.4 g (0.18 mol) of sodium nitrite were dissolved in 135 ml of ice water, to which 12.5 g (0.21 mol) of glacial acetic acid was added. The solution was added dropwise at 10 ° C over 10 minutes. The solution was stirred at 20 ° C for 1 hour and concentrated hydrochloric acid
15 ml was added and the mixture was extracted 4 times with 50 ml of ethyl acetate each. The organic layer was washed with 15 ml of ice water to neutralize, dried over sodium sulfate, and concentrated to 200 g. 3.2 g of this solution Pt / C
Hydrogenation was carried out at room temperature under a hydrogen pressure of 10 bar using a (5%) catalyst.
反応混合物を濾過し、濾液にトルエンスルホン酸一水
和物28.8g(0.15モル)をメタノール25gに溶解した溶液
を加え、120gに濃縮し、さらにトルエン200mlを加えて1
55gに濃縮した後、4℃で12時間保持した。The reaction mixture was filtered, and a solution prepared by dissolving 28.8 g (0.15 mol) of toluenesulfonic acid monohydrate in 25 g of methanol was added to the filtrate and concentrated to 120 g.
After concentrating to 55 g, it was kept at 4 ° C. for 12 hours.
沈澱したアミノシアノ酢酸エチルエステル−トシル塩
を濾別し、トルエンで洗浄した後、乾燥した。The precipitated aminocyanoacetic acid ethyl ester-tosyl salt was filtered off, washed with toluene and then dried.
酢酸エチルから再結晶し、33.7gの生成物が得られ
た。収率74.9%(シアノ酢酸エチルエステル基準)。Recrystallization from ethyl acetate gave 33.7 g of product. Yield 74.9% (based on cyanoacetic acid ethyl ester).
実施例7 ヒドロキシイミノシアノ酢酸メチルエステルからアミノ
シアンアセトアミドの製造 ヒドロキシイミノシアノ酢酸メチルエステル38.6g
(0.3モル)を200mlのメタノールに溶解し、これを3.1g
のPt/C(5%)触媒を用いて、水素圧力10バールの下、
室温で水素化した。反応混合物を濾過し、濾液に氷水15
mlを加え、これを0℃でアンモニア9.0gをメタノール25
gに溶解した溶液に添加した。この反応混合液を0℃で3
0分間撹拌した。Example 7 Preparation of aminocyanacetamide from hydroxyiminocyanoacetic acid methyl ester 38.6 g of hydroxyiminocyanoacetic acid methyl ester
Dissolve (0.3 mol) in 200 ml of methanol and add 3.1 g
With Pt / C (5%) catalyst under hydrogen pressure of 10 bar,
Hydrogenated at room temperature. The reaction mixture was filtered and the filtrate was cooled with ice water 15
ml was added, and at 0 ° C, 9.0 g of ammonia was added to methanol 25
It was added to the solution dissolved in g. The reaction mixture was stirred at 0 ° C for 3
Stirred for 0 minutes.
沈澱したアミノシアンアセトアミドを濾別し、トルエ
ンで洗浄した後、乾燥した。The precipitated aminocyanacetamide was filtered off, washed with toluene and then dried.
これにより、融点119.5〜120.5℃の生成物18.4gが得
られた。一方、濾液を150mlに濃縮し、450mlのトルエン
を加えて300mlに濃縮し、4℃で12時間保持した。沈澱
したアミノシアンアセトアミドを濾別し、トルエンで洗
浄した後、乾燥した。これから、融点112〜115℃の生成
物6.0gが得られた。This gave 18.4 g of product, mp 119.5-120.5 ° C. On the other hand, the filtrate was concentrated to 150 ml, 450 ml of toluene was added, and the mixture was concentrated to 300 ml and kept at 4 ° C. for 12 hours. The precipitated aminocyanacetamide was filtered off, washed with toluene and then dried. This gave 6.0 g of product, mp 112-115 ° C.
全体の収率:82.0%(ヒドロキシイミノシアン酢酸メ
チルエステル基準) 元素分析:C3H5N3O 計算値 C36.2%、H5.1%、N40.5% 実測値 C36.4%、H5.1%、N42.4% 実施例8 シアノ酢酸メチルエステルからアミノシアンアセトアミ
ドの製造(直接合成) シアノ酢酸メチルエステル40.0g(0.40モル)と亜硝
酸ナトリウム33.5g(0.48モル)を300mlの水に溶解し、
これに氷酢酸31.8g(0.53モル)を10℃で20分間かけて
滴下した。この溶液を20℃で1時間撹拌した後、濃塩酸
50.6g(0.5モル)を加え、各50mlの酢酸エチルで6回抽
出した。Overall yield: 82.0% (hydroxyimino cyan acid methyl ester standards) Elemental analysis: C 3 H 5 N 3 O Calculated C36.2%, H5.1%, N40.5% Found C36.4%, H5 .1%, N42.4% Example 8 Production of aminocyanacetamide from cyanoacetic acid methyl ester (direct synthesis) 40.0 g (0.40 mol) of cyanoacetic acid methyl ester and 33.5 g (0.48 mol) of sodium nitrite were added to 300 ml of water. Dissolve
To this, 31.8 g (0.53 mol) of glacial acetic acid was added dropwise at 10 ° C over 20 minutes. This solution was stirred at 20 ° C for 1 hour and then concentrated hydrochloric acid
50.6 g (0.5 mol) was added and the mixture was extracted 6 times with 50 ml of ethyl acetate each time.
有機層を各50mlの水で2回洗浄して中性にし、硫酸ナ
トリウムで乾燥した後、150mlに濃縮し、100mlのメタノ
ールを添加した。この溶液を5.1gのPt/C(5%)触媒を
用いて、水素圧力6〜10バールの下、室温で水素化し
た。The organic layer was washed twice with 50 ml of water each time to neutral, dried over sodium sulfate and then concentrated to 150 ml and 100 ml of methanol was added. The solution was hydrogenated with 5.1 g of Pt / C (5%) catalyst at room temperature under hydrogen pressure of 6-10 bar.
反応混合物を濾過し、濾液に15mlの水を加え、これを
0〜5℃でアンモニア36.7g(2.2モル)をメタノール15
0mlに溶解した溶液に添加した。1時間後に、沈澱した
生成物を濾別し、メタノールで洗浄し、乾燥した。The reaction mixture was filtered, 15 ml of water was added to the filtrate, and 36.7 g (2.2 mol) of ammonia was added to methanol at 0-5 ° C.
It was added to a solution dissolved in 0 ml. After 1 hour, the precipitated product was filtered off, washed with methanol and dried.
これにより、融点121〜122℃のアミノシアンアセトア
ミド20.4gが得られた。一方、濾液を50gに濃縮し、冷却
してもう一度濾過したところ、融点120〜121℃の生成物
8.7gが得られた。This gave 20.4 g of aminocyanacetamide with a melting point of 121-122 ° C. On the other hand, when the filtrate was concentrated to 50 g, cooled, and filtered again, the product having a melting point of 120 to 121 ° C.
8.7 g was obtained.
全体の収率:73.2%(シアノ酢酸メチルエステル基準)Overall yield: 73.2% (based on cyanoacetic acid methyl ester)
Claims (6)
たはシアノ酢酸アリールアルキルエステルを、アルカリ
金属亜硝酸塩の存在下でニトロ化して対応するヒドロキ
シイミノシアノ酢酸エステルとし、これを必要に応じて
分離し、または分離することなく直接に、白金触媒の存
在下で水素還元してアミノシアノ酢酸エステルとし、こ
れを必要に応じて分離し、または分離することなく、ア
ンモニア水と反応させて目的生成物とすることを特徴と
するアミノシアンアセトアミドの製造方法。1. A cyanoacetic acid (C 1 -C 4 ) alkyl ester or a cyanoacetic acid arylalkyl ester is nitrated in the presence of an alkali metal nitrite to give a corresponding hydroxyiminocyanoacetic acid ester, which is, if necessary, Separated or directly without separation, hydrogen reduction in the presence of a platinum catalyst to give an aminocyanoacetic acid ester, which may be separated as necessary or, without separation, reacted with aqueous ammonia to give the desired product. And a method for producing aminocyanacetamide.
ルミニウム、二酸化ケイ素、硫酸バリウム、炭酸カルシ
ウムまたは炭素からなる担体に白金を1〜20重量%担持
させたものを使用する請求項1の製造方法。2. The method according to claim 1, wherein the platinum catalyst is platinum oxide, or a carrier composed of aluminum oxide, silicon dioxide, barium sulfate, calcium carbonate, or carbon with 1 to 20% by weight of platinum supported thereon. .
〜40℃の条件下に行なう請求項1または2の製造方法。3. Hydrogenation at a pressure of 1-100 bar and a temperature of 0.
The method according to claim 1 or 2, which is carried out under the condition of -40 ° C.
ル、低級脂肪族カルボン酸エステルまたは低級脂肪族カ
ルボン酸を溶媒として用いる請求項1ないし3のいずれ
かの製造方法。4. The process according to claim 1, wherein a lower aliphatic alcohol, a lower aliphatic carboxylic acid ester or a lower aliphatic carboxylic acid is used as a solvent when hydrogenating.
で行なう請求項1ないし4のいずれかの製造方法。5. The method according to claim 1, wherein the reaction with aqueous ammonia is carried out at a temperature of −20 to 30 ° C.
のアミノシアノ酢酸エステルに対し1〜30モル当量のア
ンモニアを用いる請求項1ないし5のいずれかの製造方
法。6. The method according to claim 1, wherein 1 to 30 molar equivalents of ammonia are used per 1 molar equivalent of aminocyanoacetic acid ester in the reaction with aqueous ammonia.
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Application Number | Priority Date | Filing Date | Title |
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CH186188 | 1988-05-17 | ||
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1120230A Expired - Lifetime JP2684767B2 (en) | 1988-05-17 | 1989-05-12 | Method for producing aminocyanacetamide |
Country Status (7)
Country | Link |
---|---|
US (1) | US5003099A (en) |
EP (1) | EP0342616B1 (en) |
JP (1) | JP2684767B2 (en) |
AT (1) | ATE101124T1 (en) |
CA (1) | CA1328664C (en) |
DE (1) | DE58906866D1 (en) |
FI (1) | FI89906C (en) |
Families Citing this family (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5182385A (en) * | 1990-10-09 | 1993-01-26 | Merck & Co., Inc. | 2-biphenyl-carbapenems intermediates |
US5177202A (en) * | 1990-10-09 | 1993-01-05 | Merck & Co., Inc. | 2-phenanthrenyl-carbapenems |
US5196529A (en) * | 1990-10-09 | 1993-03-23 | Merck & Co., Inc. | 2-phenanthrenyl carbapenem intermediates |
US5132422A (en) * | 1990-10-09 | 1992-07-21 | Merck & Co., Inc. | 2-naphthyl-carbapenem intermediates |
US5132421A (en) * | 1990-10-09 | 1992-07-21 | Merck & Co., Inc. | 2-naphthyl-carbapenem intermediates |
US5144028A (en) * | 1990-10-09 | 1992-09-01 | Merck & Co., Inc. | 2-(9-fluorenonyl)-carbapenem intermediates |
US5356889A (en) * | 1990-08-01 | 1994-10-18 | Merck & Co., Inc. | 2-(9-fluorenonyl)-carbapenem intermediates |
US5208329A (en) * | 1990-10-09 | 1993-05-04 | Merck & Co., Inc. | 2-biphenyl carbapenem intermediates |
CH692506A5 (en) * | 1997-12-18 | 2002-07-15 | Eprova Ag | A process for producing aminocyanoacetamide. |
US6194600B1 (en) | 1997-12-18 | 2001-02-27 | Eprova A.G. | Method of producing aminocyanoacetamide |
US6090970A (en) * | 1998-06-19 | 2000-07-18 | Sumika Fine Chemicals Co., Ltd. | Production method of alkylated cyanoacetylurea |
EP1353924A1 (en) * | 2001-01-18 | 2003-10-22 | Schering Corporation | Synthesis of temozolomide and analogs |
CN116444399A (en) * | 2023-04-26 | 2023-07-18 | 济南大学 | Method for synthesizing (2E) -2-cyano-2-hydroxy iminoacetic acid ethyl ester by micro-reaction |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2367455A (en) * | 1941-04-09 | 1945-01-16 | Rohm & Haas | Aminocyanoacetamide resins |
JPS5221326A (en) * | 1975-08-11 | 1977-02-17 | Takeda Chem Ind Ltd | Plant disease controlling agent |
CH597162A5 (en) * | 1976-01-13 | 1978-03-31 | Lonza Ag | |
US4328171A (en) * | 1979-11-26 | 1982-05-04 | The Dow Chemical Company | Preparation of cyanoacetamide and 2,2-dibromo-3-nitrilopropionamide compositions |
CH673647A5 (en) * | 1987-06-09 | 1990-03-30 | Lonza Ag |
-
1989
- 1989-04-05 FI FI891625A patent/FI89906C/en not_active IP Right Cessation
- 1989-05-05 US US07/348,054 patent/US5003099A/en not_active Expired - Fee Related
- 1989-05-10 CA CA000599341A patent/CA1328664C/en not_active Expired - Fee Related
- 1989-05-12 JP JP1120230A patent/JP2684767B2/en not_active Expired - Lifetime
- 1989-05-16 EP EP89108794A patent/EP0342616B1/en not_active Expired - Lifetime
- 1989-05-16 AT AT89108794T patent/ATE101124T1/en not_active IP Right Cessation
- 1989-05-16 DE DE89108794T patent/DE58906866D1/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP0342616A3 (en) | 1991-06-05 |
US5003099A (en) | 1991-03-26 |
CA1328664C (en) | 1994-04-19 |
DE58906866D1 (en) | 1994-03-17 |
EP0342616A2 (en) | 1989-11-23 |
FI89906B (en) | 1993-08-31 |
FI891625A0 (en) | 1989-04-05 |
ATE101124T1 (en) | 1994-02-15 |
FI891625A (en) | 1989-11-18 |
JPH0217162A (en) | 1990-01-22 |
EP0342616B1 (en) | 1994-02-02 |
FI89906C (en) | 1993-12-10 |
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